CATALYST COMPOSITION FOR PREPARATION OF POLYETHYLENE PROCESS FOR PREPARATION OF CATALYST PRECURSOR AND PROCESS FOR (CO-)POLYMERIZATION OF ETHYLENE

摘要

1. Catalyst composition for the (co-)polymerisation of ethylene optionally with an alpha olefin of 3 to 10 carbon atoms, comprising a catalyst precursor and an organoaluminium cocatalyst, wherein the catalyst precursor consists of: (i) a silica carrier material, having from 0.3 to 1.2 mmoles of OH groups per gram of silica, (ii) a dialkylmagnesium compound of the formula RMgR1, where R and R1 are the same or different C2 -C12 alkyl groups, in an amount between 0.5 and 1.5 mmoles of dialkylmagnesium per gram of silica, (iii) a tetraalkyl orthosilicate, in which each of the alkyl groups contains from 2 to 6 carbon atoms, in an amount between 0.2 and 0.8 mmoles of tetraalkyl orthosilicate per gram of silica, (iv) a chlorinated compound (X) having the formula RnSiCl4-n, wherein each R is the same or different and is hydrogen or an alkyl group and n is an integer from 0 to 3, in an amount between 0.2 and 4 mmoles of X per gram of silica, and (v) a titanium compound in an amount between 0.3 and 1.5 mmoles per gram of silica. 2. Catalyst composition according to claim 1 wherein the silica carrier material has from 0.3 to 0.7 mmoles of OH groups per gram of silica. 3. Catalyst composition according to claims 1 to 2 wherein the dialkylmagnesium compound is butylethylmagnesium, butyloctylmagnesium, dibutylmagnesium, or mixtures thereof. 4. Catalyst composition according to claim 3 wherein the dialkylmagnesium compound is dibutylmagnesium. 5. Catalyst composition according to claims 1 to 4 wherein the tetraalkyl orthosilicate is tetraethoxysilane, tetraisopropoxysilane, tetrapropoxysilane, tetrabutoxysilane, and mixtures thereof. 6. Catalyst composition according to claim 5 wherein the tetraalkyl orthosilicate is tetraethoxysilane. 7. Catalyst composition according to claimsw 1 to 6 wherein the organoaluminium cocatalyst is dimethyl-aluminiumchloride, trimethylaluminium, triisobutylaluminium, triethylaluminium, and mixtures thereof. 8. Catalyst composition according to claim 7 wherein the organoaluminium cocatalyst is triethylaluminium. 9. Catalyst composition according to claims 1 to 8 wherein the titanium compound is a tetravalent titanium compound or any mixtures thereof. 10. Catalyst composition according to claim 9 wherein the titanium compound is titanium tetrachloride. 11. Catalyst composition according to claims 1 to 10 wherein the chlorinated compound (X) has the formula RnSiCl4-n, wherein each R is the same or different and is hydrogen or a C1-C12 alkyl group and n is an integer from 0 to 3. 12. Catalyst composition according to claim 11 wherein the chlorinated compound (X) is selected from the group consisting of silicon tetrachloride, methyl trichlorosilane and mixtures thereof. 13. Catalyst composition according to claim 12 wherein the chlorinated compound (X) is silicon tetrachloride. 14. Process for the preparation of a catalyst precursor which comprises the steps of: (1) reacting a silica carrier material, having from 0.3 to 1.2 mmoles of OH groups per gram of silica, with a dialkylmagnesium compound of the formula RMgR1, where R and R1 are the same or different C2-C12 alkyl groups, in an amount between 0.5 and 1.5 mmoles of dialkylmagnesium per gram of silica, in order to form a silica supported organomagnesium composition, (2) reacting said silica supported organomagnesium composition with a tetraalkyl orthosilicate, in which each of the alkyl groups contains from 2 to 6 carbon atoms, in an amount between 0.2 and 0.8 mmoles of tetraalkyl orthosilicate per gram of silica, (3) contacting the product from step (2) with a titanium compound in an amount between 0.3 and 1.5 mmoles per gram of silica, said preparation process further including the additional step of contacting either the product from step (1), or the product of step (2), or the silica support directly with a chlorinated compound (X) having the formula RnSiCl4-n, wherein each R is the same or different and is hydrogen or an alkyl group and n is an integer from 0 to 3, in an amount of from 0.2 to 4 mmoles of X per gram of silica. 15. Process according to claim 14 wherein the total addition of the chlorinated compound (X) is performed after the addition of the tetraalkyl orthosilicate and before the addition of the titanium compound. 16. Process for (co-)polymerization of ethylene optionally with an alpha olefin of 3 to 10 carbon atoms wherein using the catalyst according to any claim 1 to 13.